Classifications

• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
  • D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
  • D21C5/02—Working-up waste paper
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
  • D21H21/02—Agents for preventing deposition on the paper mill equipment, e.g. pitch or slime control
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
  • D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
  • D21C9/08—Removal of fats, resins, pitch or waxes; Chemical or physical purification, i.e. refining, of crude cellulose by removing non-cellulosic contaminants, optionally combined with bleaching
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
  • D21H23/78—Controlling or regulating not limited to any particular process or apparatus
• • G—PHYSICS
  • G01—MEASURING; TESTING
  • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
  • G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
  • G01N33/34—Paper
  • G01N33/343—Paper paper pulp

Definitions

• the invention relates to a method and a system for continuously and automatically determining sticky levels in a process for producing recycled fibre pulp utilizing near-infrared (NIR) spectroscopy in combination with one or more automated sheet former (s) .
• NIR near-infrared
• Stickies are grouped into primary and secondary stickies
• Stickies may originate from a variety of different sources such as adhesives applications from various paper products, hotmelts from bookbinders and carton sealants, self adhesive labels, polymeric binders from coated paper and ink residues . Stickies typically are classified as hot melts, pressure-sensitive adhesives (PSAs) , latexes, binders, pitch, and ink and
• Stickies can also be classified as
• Stickies may cause operational and product quality problems. Stickies can deposit on surfaces of the paper machine equipment, such as wires, felts, press rolls, and drying cylinders, cause process upsets, hinder fiber bonding, and reduce product
• stickies may cause bright and dark spots in the paper or even sheet breaks, which results in lower paper quality, production losses and extra operating stops for
• the amount of stickies in the recycled pulp may be reduced by, e.g., optimization of re-pulping parameters, cleaning and screening, flotation, dispersing and chemical treatment.
• Usual chemical treatments to reduce stickies or to reduce their sticky character are dispersion and/or passivation of the stickies by addition of e.g. talc and/or bentonite, chemical detacifiers, e.g. polymers, and treatment of the process equipments with chemicals to retard the deposition. These chemical treatments contribute significantly to operating costs.
• microstickies are stickies that pass a 100 ⁇ slotted plate in laboratory screening.
• Macrostickies are defined as the stickies in the residue of the 100 m screen.
• the standard laboratory analytical procedures for determining sticky levels allow the determination of either micro-, macro- or both types of
• macrostickies can be monitored using a device known as a "Pulmac shive analyzer” or “Haindl fractionator” , which screens out the macrostickies from the furnish and
• NIR near infrared
• the present invention relates to a method of continuously and automatically determining sticky levels in a process for
• NIR near- infrared
• automated sheet former which comprises the steps: (a) determining sticky levels for a series of samples using a standard laboratory analytical procedure, utilizing the results as reference values to establish one or more calibration model (s) from NIR spectroscopy, and storing the dataset(s) of the calibration model (s) on an electronic storage device;
• step (b) automatically withdrawing a sample from at least one sampling point in the process line, transporting the sample through a sample line from the process line to at least one automated sheet former, forming a sheet from said sample, and drying said sheet; (c) transporting the dried sheet from step (b) to a measuring zone and recording a spectrum from the sheet in the near infrared region to obtain spectral data;
• step (d) processing the spectral data obtained in step (c) on a computer utilizing at least one stored calibration model, and receiving for each calibration model as output a value of the sticky level in the process for producing recycled fibre pulp.
• the method of the invention makes it possible to monitor and control the amounts of stickies in real-time in the process of producing recycled pulp.
• the method allows the process of producing recycled pulp to be controlled in a feed- forward manner in order to reduce the amount of stickies and/or adjust the process to thereby minimize negative effects of the stickies on the production process, e.g. reject rates and/or chemical dosages .
• the method can be used in any conventional process for producing recycled fibre pulp, which process, for example, comprises the steps of pulping recovered paper and cleaning the resulting fiber suspension, e.g. by screening, centrifugal cleaning and/or flotation.
• the near infrared (NIR) calibration models may be established by calibrating reference spectral data, obtained by spectrometric measurements in the near infrared range on reference samples, to known sticky values of said reference samples by means of partial least squares regression.
• Spectral measurements are made on the formed sheets by use of a NIR spectrometer, such as a Fourier Transform Near Infrared spectrometer.
• the spectrometer may comprise a fiber-coupled measurement head for contactless measurements on the sheet.
• the spectral measurements are performed in the near- infrared spectral region, most preferably in the wavelength range of 833 to 2564 nm or 12000 to 3900 cm “1 .
• Spectral data is collected by means of transmission or reflectance for each formed sheet, preferably reflectance. In this way, spectral data is obtained for each sheet.
• the multivariate data analysis may be carried out using e.g. partial least squares regression
• Multivariate analysis is based on the statistical principle of multivariate statistics, which involves observation and analysis of more than one statistical outcome variable at a time. This statistical technique allows to take into account the effects of all variables on the responses of interest, e.g. data from different sampling points and/or machine and process parameters .
• the known sticky values of the reference samples are the amounts of stickies in the samples as determined by means of standard laboratory analytical procedure for determining stickies, including reference methods such as Ingede method No. 4 ,
• Kaipola sticky method extraction by means of dimethylformamide (DMF) , tert-butyl methyl ether (TBME) or dichloromethane (DCM) , flow cytometry, addition of deposits of the doctor blades of the paper machine to pulp samples, or addition of industrial adhesives to pulp samples .
• DMF dimethylformamide
• TBME tert-butyl methyl ether
• DCM dichloromethane
• the sticky values of the reference samples as determined by the individual standard laboratory analytical reference methods and the spectroscopic data of the reference samples are used as input for a correlation to create a calibration model for each standard laboratory analytical reference method. Accordingly, it is possible to predict stickies levels for various kinds of stickies by processing obtained spectroscopic data from a sample utilizing one or more calibration model (s) .
• the spectroscopic data of a single NIR spectrum from a single sample can be utilized as input in one or more of the calibration models thereby yielding as output one or more sticky value (s) as determined with each of the respective laboratory analytical reference methods forming the basis of the individual
• the second model can be used to predict or determine a value, which value expresses the adverse effects of the stickies on the production process, e.g. paper quality defects and/or problems at the paper machine, e.g. deposits on paper machinery, web breaks, holes and spots.
• This value of the second model is also referred to as sticky
• Historical data of process conditions and machinery settings may also be used as additional values that can be taken into account for predicting the sticky disturbing potential, due to the fact that those parameters can affect the harmfulness of stickies, e.g. pH value and ash content of the pulp or temperature profiles of the drying cylinders of the paper machine .
• a first sticky value may e.g. be determined by use of flow cytometry and a second sticky value may e.g. be determined by means of the Kaipola sticky method. Then the output data of these methods are combined and weighted according to their relative impact on the runability of the paper machine to thereby create a sticky disturbing potential.
• the different reference methods can express different types or different sizes of stickies.
• machine/process may be determined by means of multivariate data analysis. This can, e.g., be accomplished by creating a second multivariate model wherein the weight of the variables
• the variables expressing the amounts of stickies may be the predicted sticky values
• the second model may further comprise other process and pulp parameters, e.g. pH value and ash content of the pulp, temperature profiles of the drying cylinders of the paper machine .
• the second model can be used to determine the sticky disturbing potential of new samples, collected on-line in the process as explained above.
• the predicted sticky disturbing potential values are thereafter used to regulate the process, e.g. by regulating the reject rates of screens or steering the amount of chemicals added to the fiber suspension.
• one or more means an integer of from 1 to 50, preferably an integer of from 1 to 15, more preferably 1, 2, 3, 4, 5, 6, 7, or 8.
• the method of the invention can also be characterized in that the method further comprises the step of measuring the weight of the sheet after recordation of the NIR spectrum.
• the method of the invention can also be characterized in that the calibration model is established by calibrating reference spectral data, obtained by spectrometric measurements in the near infrared region on reference samples, to known sticky values of said reference samples by means of multivariate data analysis .
• the method of the invention can be characterized in that at least one sample from at least one sampling point in the process line is withdrawn every hour. Preferably at least one sample from at least one sampling point in the process line is withdrawn at least every 30 min, more preferably at least every 15 min, and most preferably about every 5 to 12 min. According to the method of the invention it is possible to withdraw individual samples at defined sampling points in the process line at certain time intervalls, e.g. at least one sample per hour, at least one sample every 30 min, at least one sample every 5 to 15 min.
• the method of the invention can also be characterized in that the process for producing recycled fibre pulp utilizing near- infrared (NIR) spectroscopy in combination with an automated sheet former comprises at least one of the following process steps: pulping, high density (HD) cleaning, pre-screening, high weight (HW) cleaning, intermediate consistency (IC) screening, pre-flotation, fine screening, thickening (i.e. water is removed from the pulp, e.g. using a disk filter), dewatering (i.e. water is removed from the pulp, e.g. by channeling the pulp through a screw press or double wire press), dispersion (i.e.
• NIR near- infrared
• thermo- mechanical treatment of the pulp to reduce the size of stickies e.g., post-flotation, thickening, dewatering, stock tower (i.e. a tank located between a deinking plant and a paper machine where the deinked pulp is stored) , or combinations thereof .
• the method of the invention can also be characterized in that the process for producing recycled fibre pulp utilizing near- infrared (NIR) spectroscopy in combination with an automated sheet former has the following process arrangement: pulping, HD cleaning, pre-screening, HW cleaning, IC screening, pre- flotation, fine screening, thickening, dewatering, dispersion, post-flotation, thickening, dewatering, and stock tower, in that order .
• NIR near- infrared
• a sample can be withdrawn from one or several sampling points in the process line.
• the sampling point in the process line can be selected from the sampling points: immediately downstream of the pre-screening, immediately downstream of the HW cleaning, immediately downstream of the IC screening, immediately downstream of the pre- flotation,
• the reject rates can be controlled in a feed-forward manner .
• One sample may, e.g., be withdrawn in advance of, i.e. upstream of, at least one screener. At this sampling point, the fiber suspension contains a large amount of macrostickies but also microstickies .
• a second sampling point may, e.g., be after the deinked pulp storage tower, wherein the fiber suspension contains still macro-, and microstickies but on a lower level.
• a third sampling point may be the head box of the paper machine, wherein the pulp suspension also contains secondary stickies.
• samples may be taken from a combination of sample points, e.g. the three sampling points mentioned above, with a certain time shift depending on the sheet former capacity.
• the method of the invention can be characterized in that samples are withdrawn from at least two sampling points in the process line, more preferably from at least three sampling points in the process line. This makes it possible to monitor and control different kinds and sizes of stickies, e.g. macro- and
• microstickies at different positions in the process line.
• the method utilizes one or more standard analytical procedure (s) to create (a) respective calibration model (s).
• the standard analytical procedure (s) is/are selected from: Ingede method No. 4, Kaipola sticky method, extraction by means of dimethylformamide (DMF) , tert-butyl methyl ether
• the INGEDE method 4 describes a laboratory screening procedure for pulps of a recovered paper treatment process. The reject of this screening procedure over a 100 ⁇ slotted plate is prepared in such a way that the macro stickies can be determined by means of an image analysis system. The obtained values are the macro sticky area expressed as mm 2 per kg pulp. Specifically, the Ingede method No. 4 is an established method for the
• the Kaipola sticky method also describes a laboratory screening procedure but after screening the macro sticky area is
• the Kaipola sticky method comprises the following steps:
• the pulp is disintegrated in in lab disintegrator according to ISO 5263-1.
• the disintegration of 50 g bone dry pulp is performed at 3000 rpm and 2 % consistency for 10 minutes. Otherwise the fibre flakes may disturb the
• the screening is done with a Somerville screen (TAPPI T 275 sp- 07) , in which 50 g bone dry pulp are screened for 20 minutes with a 100 m slotted plate.
• the residual over the screen plate is transferred to a white filter paper of 110 mm diameter, covered with an aluminum foil, loaded with a heated metal plunger (130 mm diameter, 2.8 kg) and dried on an oven plate.
• the temperature of the plate is 100 to 110 °C and drying is performed until the filter paper becomes slightly brown, which takes about 10 minutes.
• Additional white filter papers should be used if there is an overlapping of residuals on the filter paper. This means the residues of the slotted plate have to be split up to more than one filter paper before drying them.
• the aluminum foil is released after the drying.
• a rewetting of the filter paper, on which the residuals are located, is done with tap water.
• the wet filter paper is placed on a black surface on which the stickies are visible as white spots.
• the sticky amount (white spots) is estimated by numbers and size manually using the transparent reference foil shown in Fig. 10 (scaled) .
• the transparent foil is placed over the wetted filter paper and the stickies are classified and compared with the areas on the foil according to Table A below.
• the number of stickies per class is cumulated and multiplied by the average area of each size class of stickies. The result is then
• Flow cytometry comprises the following steps:
• the diluted sample of step 2 is in a first step filtrated with a Britt Dynamic Drainage Jar (BDDJ) using a metal screen of 150 mesh according to a hole diameter of 106 ⁇ and in a second filtration step the sample is fine screened using a 80 ⁇ hole diameter filter in order not to plug the cuvette of the flow- cytometer .
• BDDJ Britt Dynamic Drainage Jar
• step 3 The filtrate of step 3 is diluted by ten times (1:10) using Milli-Q-water to obtain a base dilution.
• a test sample of 1 ml is prepared by mixing 50 ⁇ of the base dilution with 950 ⁇ Milli-Q-water in a cuvette (i.e. a further dilution of 1:20). 20 ⁇ nile red (0.001% in methanol) is added to the test sample to obtain a cuvette sample.
• the cuvette sample is stored in
• the cuvette sample is mixed with a vortex generator (e.g. TopMix FB15024 (Fisher Scientific)) for 15 seconds at an intensity of 25 Hz to ensure a homogeneous sample.
• the count rate of the cuvette sample is adjusted to 900-1100 counts/sec in a flow-cytometer (if the cuvette sample does not have a count rate of 900-1100 counts/sec, the base dilution needs to be adapted accordingly to achieve a count rate of 900- 1100 counts/sec and the measurement has to be repeated) .
• the total amount of hydrophobic sticky particles in the cuvette sample of step 4 is determined with a flow-cytometer, e.g. Cyflow SL ® (by Partec) equipped with a 488 nm blue solid state laser and 5 optical parameters (forward scatter (FSC) , side scatter (SSC) , detector sensitive for wave length of green light (FL1) , detector sensitive for wave length of orange light (FL2) , detector sensitive for wave length of red light (FL3)) using the parameter settings shown in Table B.
• the measuring time is approximately 180-220 seconds measuring a constant volume of 0.2 ml. About 200.000 particles are recorded with these settings.
• the FSC channel is used as triggering channel with a sample flow speed of 2.5 ⁇ /sec. Table B.
• Extraction methods deliver the amount of pulp components soluble in appropriate solvents, e.g. dimethylformamide (DMF) , tert- butyl methyl ether (TBME) or dichloromethane (DCM) expressed as percentage of soluble material.
• appropriate solvents e.g. dimethylformamide (DMF) , tert- butyl methyl ether (TBME) or dichloromethane (DCM) expressed as percentage of soluble material.
• DMF dimethylformamide
• TBME tert- butyl methyl ether
• DCM dichloromethane
• dichloromethane DCM
• DCM dichloromethane
• Latex 5,1 Standard newsprint paper was then pulped using a Hobart pulper at 20 % consistency with addition of 0,6 % NaOH, 1,8 % silicate and 0,7 % peroxide.
• the share of adhesives relative to the pulp was defined (0 to 10 %) and the needed amount of adhesive application mixture was calculated and mixed properly with the pulped newsprint paper. Subsequently funnel sheets were formed and dried as described in the INGEDE method 1
• Deposits of the doctor blades of the paper machine were cooled down by using liquid nitrogen, crushed and then added to pulp samples with a mass share of 0 to 20 percent whereof sheets were formed for spectroscopic measurements.
• deposits of the doctor blades of the paper machine were collected. Due to the sticky properties the deposits were cooled down with liquid nitrogen to make the material more brittle and to be able to reduce the particle size.
• the sample was treated mechanically by using a standard porcelain mortar with continuous addition of liquid nitrogen to keep the temperature on a low level for about 15 minutes.
• the prepared sample material with particle sizes of 150 to 500 ⁇ was then kept in a freezer at -20°C to prevent re- agglomeration of the particles.
• Standard newsprint paper was pulped using a Hobart pulper at 20 % consistency with addition of 0,6 % NaOH, 1,8 % silicate and 0,7 % peroxide. Defined masses of the deposits (0 to 20 % related to the funnel sheet weight) were then added to the pulp suspension and stirred properly. Subsequently funnel sheets were formed and dried as described in the INGEDE method 1
• the NIR calibration models are validated by use of reference samples with known content of stickies as determined by one or more standard analytical procedure (s) .
• the method of the invention can further be characterized in that the method further comprises a step for controlling the sticky levels in the process for producing recycled fibre pulp from recovered paper based on the determined value of the sticky levels according to step (d) .
• the method can be characterized in that the step for controlling the sticky levels in the process for producing recycled fibre pulp from recovered paper comprises: adjusting the reject rate of at least one screener, regulating the
• adjusting the disperser settings i.e. changing the mechanical energy that is put in the pulp by using a rotor and stator equipped with teeth, e.g. by closing or opening the gap between rotor or stator; or by changing the consistency of the pulp
• chemicals added in relation to the amount of stickies for example, if the sticky amount is very low, the amount of chemicals can be reduced thereby saving costs and preserving the environment) , which chemicals have an effect of passivation, stabilisation, detackification, fixation or reducing the content of the stickies in the pulp.
• the invention further pertains to a system for continuously and automatically determining sticky levels in a process for
• NIR near- infrared
• spectrometer to perform spectroscopic measurements on the formed sheets in the NIR region; and a computer programmed to carry out multivariate data analysis.
• the system according to the invention makes it possible to continuously and automatically monitor the amount of stickies in the fiber suspension in real-time. Moreover, the method and system of the invention allow simultaneous determination of values for various kinds of stickies by processing the spectral data obtained for the individual sample (s) of the process for producing recycled fibre on a computer utilizing one or more of the calibration models, alone or in combination.
• Figure 1 shows a graphic representation of single values of bright and dark spots observed in the production of a paper over a certain time period.
• Figure 2 shows a graphic representation of breaks observed in the production of a paper over a certain time period.
• Figure 3 shows a CUSUM chart created for the values of bright and dark spots depicted in Fig. 1.
• Figure 4 shows a CUSUM chart created for the breaks depicted in Fig. 2.
• Figure 5 shows a correlation of predicted sticky values
• Adhesives V2 to the number of bright and dark spots observed in the production of a paper.
• Figure 6 shows a correlation of predicted sticky values
• Figure 7 shows a correlation of predicted sticky values
• Figure 8 shows a correlation of the combined sticky values according to the calibration models FCM VI and Adhesives V2 to the number of bright and dark spots observed in the production of a paper.
• Figure 9 shows a correlation of predicted values (intensely serrated grey line) and measured values (dark zigzag line) for bright and dark spots observed in the production of a paper.
• Figure 10 shows a pattern (scaled) for manually determining the sticky amount.
• the pattern is put on a transparent reference foil and the sticky amount (white spots) is estimated by
• the calibration models based on the NIR measurements of said reference samples and the measured amounts of stickies were created by means of PLS using the software OPUS supplied by Bruker Optik GmbH.
• For each sticky reference method two separate NIR calibration models were established using different spectral pre treatment methods and spectral ranges (below referred to as version 1 (VI) and version 2 (V2) .
• the calibration models were tested using an internal cross validation and external
• a sticky disturbing potential as indicator for the runability of the paper machine had to be defined.
• the sticky disturbing potential is a value which expresses the adverse effects of the stickies on the production process, e.g. paper quality defects and/or problems at the paper machine, e.g. deposits on paper machinery, web breaks, holes and spots.
• the number of breaks is non-normal distributed and shows a high variation ( Figure ) thus using single values for the number of web breaks per day as sticky disturbing potential did not result in a good model.
• Bright and dark spots in the paper are monitored continuously ⁇ Fig. 1) and expected to correlate with the number of web breaks based on experience .
• the number of breaks at the paper machine and the number of bright and dark spots were transformed using the CUSUM method to be able to correlate changes of those values.
• the CUSUM (or cumulative sum control chart) is a sequential analysis technique developed by E. S. Page of the University of Cambridge. It is typically used for monitoring change detection. By using this method the number of breaks could be correlated to the number of bright and dark spots in the same time period using historical data as shown in Fig. 3 and Fig. 4. A very good correlation could be observed .
• Fig. 5 shows the correlation of three single sticky values and the number of bright and dark spots (CUSUM) created using the software Minitab supplied by ADDITIVE GmbH.
• Fig. 8 shows the improvement when the predicted values FCM VI and Adhesives V2 are taken into consideration. The coefficient of determination is 0.87, and thus a very good prediction of bright and dark spots in the paper which is correlating to the number of breaks at the paper machine is possible just by using the above mentioned combination of sticky values.
• the sticky disturbing potential expressing the weighted mean of amounts of stickies and process parameters can be calculated using a quadratic polynomial, wherein the individual sticky values and process parameters each represent a variable Xi, x 2 , x 3 ... , x n .
• the corresponding quadratic polynomial is the quadratic polynomial
• Equation 1 Equation 1
• a represents the coefficient of the constant term
• b t represent coefficients of the linear terms
• c tj represent
• the second model can be used to determine the sticky disturbing potential of the current process conditions, and thus is a tool to improve the runability of the paper machine.
• the runability of the paper machine can be improved by considering the influence of single parameters on the creation of bright and dark spots in the paper, i.e. breaks at the paper machine, and by adjusting the process conditions or chemical additions to counteract a high sticky disturbing potential .

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• 2013
  • 2013-04-16 WO PCT/EP2013/001124 patent/WO2013156147A1/en active Application Filing
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